EP0466392B1 - Synthese von hydrophoben alkoxylierten Polymeren - Google Patents

Synthese von hydrophoben alkoxylierten Polymeren Download PDF

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EP0466392B1
EP0466392B1 EP91306039A EP91306039A EP0466392B1 EP 0466392 B1 EP0466392 B1 EP 0466392B1 EP 91306039 A EP91306039 A EP 91306039A EP 91306039 A EP91306039 A EP 91306039A EP 0466392 B1 EP0466392 B1 EP 0466392B1
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polymer
amine
hydrophobic
alkoxylated
process according
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EP0466392A2 (de
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Dodd W. Fong
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ChampionX LLC
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Nalco Chemical Co
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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F8/00—Chemical modification by after-treatment
    • C08F8/30—Introducing nitrogen atoms or nitrogen-containing groups
    • C08F8/32—Introducing nitrogen atoms or nitrogen-containing groups by reaction with amines

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  • the present invention is in the technical field of polymer synthesis by post-polymerization derivatization.
  • Polymers prepared by the polymerization of relatively simple, ethylenically-unsaturated monomers such as (meth)acrylic acid and its esters, (meth)acrylamide, maleic anhydride or maleic acid, crotonic acid and its esters, methyl vinyl ether, vinyl acetate, acrylonitrile, styrene and the like, are well known and are relatively easy to prepare by polymerization techniques well known in the art.
  • the preparation of polymers that contain hydrophobic pendant groups by the polymerization of ethylenically-unsaturated monomers which contain such hydrophobic groups using conventional polymerization techniques is limited by the availability of such monomers and possible complications arising in the attempt to incorporate such monomers into the polymer during the polymerization. Complications during the polymerization may well occur if the hydrophobe-containing monomer does not have solubility characteristics that are compatible with the desired polymerization technique(s).
  • Post-polymerization derivatization of polymers prepared by conventional polymerization techniques using relatively simple and readily available monomers, whereby a mixture of pendant hydrophobic groups and pendant alkoxylated groups, are introduced into the polymer avoids the difficulties regarding monomer availability and the complications encountered in incorporating such unusual monomers during a polymerization reaction.
  • Such a post-polymerization process is highly desirable if it is economically efficient. Economic efficiency is dependent upon many variables, including the efficiency with which the process proceeds, the reasonableness of the reaction conditions required, the availability of both the basic polymer(s) to be derivatized and the derivatizing agent(s), the use of a minimum of reaction steps and the ease at which the end product polymer can be recovered from the reaction mixture.
  • Polymers having unique mixtures of pendant hydrophobic groups and pendant alkoxylated groups are highly desirable given the unique properties imparted to the polymer by the combinations of such diverse groups.
  • a minimum number of reaction steps is desirable as is also minimum time required for the derivatization.
  • the process should preferably proceed under relatively mild reaction conditions and minimize any deleterious effects on the polymer structure.
  • the present invention also provides a unique polymer having incorporated thereinto mixtures of hydrophobic and alkoxylated pendant groups.
  • the present invention provides a method of preparing polymers having bonded to the polymer backbone pendant groups having the structural formula wherein n is zero or an integer of 1 to 10, R1 is (over the whole polymer) a mixture of both hydrophobic groups and alkoxylated groups and R is hydrogen or substituent other than hydrogen, by derivatization of a pre-existing polymer with at least one amine, in a substantially homogeneous reaction mixture at an elevated temperature for a time sufficient for (trans)amidation to occur.
  • the derivatization process employs pre-existing polymers that contain pendant groups having the structure of Formula I: wherein n is zero or an integer from 1 to about 10, and X is -NH2, -OH, or -O-, and salts thereof, and mixtures or combinations of such pendant groups.
  • salts alkali metal salts, alkaline earth metal salts, ammonium salts, amine salts and, alkanol amine salts.
  • the derivatization process employs as the source of hydrophobic and alkoxylated radicals,primary and secondary amines containing the desired radical(s).
  • the reaction mixture is comprised of the reactants, i.e. , the polymer(s) and the amine(s), and a reaction medium in which the reactants are soluble or substantially homogenously dispersible.
  • a reaction medium in which the reactants are soluble or substantially homogenously dispersible.
  • an aqueous reaction medium is employed.
  • the pendant groups subject to derivatization are contained in a polymer "unit” or “mer unit” (a segment of the polymer having two adjacent backbone carbons) having the structure of Formula II: wherein R1, R2 and R3 are independently hydrogen or substituent other than hydrogen and wherein Y is the pendant group(s) the structure of which is defined above by Formula I.
  • substituted is meant herein a single or multivalent radical other than hydrogen covalently bonded to a carbon or nitrogen of the referenced molecule.
  • R1, R2 and/or R3 of Formula II above are substituents other than hydrogen, typically they are C1 ⁇ 4 alkyl or carboxylic substituents.
  • the derivatization process is a (trans)amidation reaction whereby the hydrophobic and alkoxylated radicals of the end product polymer are substituents to the nitrogen of an acid amide group, as discussed in more detail below.
  • the present invention also provides unique polymers that contain both hydrophobic and alkoxylated pendant groups which are substituents to the nitrogen of an acid amide group, as discussed in more detail below.
  • the polymers employed in the derivatization process contain pendant groups having the structure of Formula I above and include pendant groups having carboxyl, carboxylate, and acid amide moieties. Such moieties are the reactive groups that enter the (trans)amidation reaction with the amine derivatiziting agents. There is no theoretical minimum of mer units containing such groups required of the polymer employed and the derivatization theoretically can be accomplished with as little as one such mer unit per polymer molecule.
  • the starting material polymer should have 10 mole percent or more of mer units containing the pendant groups having the structure of Formula I above.
  • Ethylenically-unsaturated monomers that provide to a polymer pendant groups having the structure of Formula I include (meth)acrylamide, (meth)acrylic acid and salts thereof, crotonic acid, maleic acid, maleic anhydride and other monomers, for instance acrylonitrile, (meth)acrylic acid esters, and the like, that may be converted into mer units having the desired final pendant groups after incorporation into the polymer, for instance by hydrolysis.
  • Polymers that may be employed in the derivatization process may contain any amount of mer units other than those providing pendant groups of Formula I above,provided that such other mer units do not comprise the entirety of the polymer. As mentioned above, however, it is believed that to achieve a favorable reaction without employing any significant excess of derivatizing agent, and to provide an end product polymer having a reasonable degree of properties derived by virtue of the derivatization, the amount of mer units not providing pendant groups of the Formula I'above should not exceed about 90 mole percent.
  • any monomer that is polymerizable with the monomers providing pendant groups of the Formula I above may be incorporated into the polymer, although considerations such as ease of polymerization of the given monomer mixture, and the propensity of the comonomers to engage in side reactions or interfere with the derivatization reaction, may be factors in the selection of comonomers.
  • vinyl acetate is generally considered a good comonomer with maleic anhydride but not with acrylic acid, and hence its desirability as a comonomer is dependent upon the type of monomer that will be providing the necessary pendant groups.
  • Other good comonomers with maleic anhydride are methyl vinyl ether or styrene.
  • Good comonomers with acrylic acid and acrylamide include the alkyl esters of acrylic acid and acrylonitrile.
  • Other possible considerations concerning the selection of suitable comonomers are the properties of the starting material polymer and the end material polymer. For instance, a hydrophilic comonomer may be preferred when it is desired to increase the water solubility of the starting material polymer and/or the end material polymer, or a hydrophobic comonomer may be selected to decrease water solubility when desired.
  • An amount of butyl acrylate may be used as a comonomer to provide a degree of tack to the end product polymer.
  • One comonomer may be more advantageous than another if the monomer itself is less toxic and the toxicity of residual monomer in the end product polymer is a consideration for the intended use of the polymer.
  • the starting material polymer may be a random polymer, or other than a random polymer.
  • the derivatizing agents are mixtures of primary and/or secondary amines having a hydrophobe radical, with primary and/or secondary amines having alkoxylated radicals.
  • the methyl radical of methyl amine is a hydrophobic radical, particularly considering the diminished hydrophilicity when a pendant acid amide group (-CONH2) is derivatized to an N-substituted methyl amide group (CONHCH3).
  • Hydrocarbon radicals having three or more carbon atoms are significantly hydrophobic for purposes of the present invention, and hydrophobic radical having 12 or more carbon atoms are preferred for some purposes of the present invention.
  • the hydrophobic radical need not be saturated, and for some purposes of the present invention a degree of carbon-to-carbon unsaturation is preferred for long-chain hydrophobic radicals.
  • the hydrophobic radical may contain other substituents provided that such substituents do not destroy the hydrophobic nature of the radical. While primary amines are preferred, the use of secondary amines is not excluded.
  • Alkoxylated radicals generally contain ethoxy (-CH2CH2O-) groups or propoxy (-CHCH3CH2O-) groups, generally derived from ethylene oxide and propylene oxide, or mixtures of both types of alkoxy groups.
  • the alkoxylated amine derivatizing agent should contain an amino group, preferably a primary amino group, and at least one alkoxyl group, and may contain other groups, for instance hydrocarbon groups.
  • a very useful group of commercially available alkoxylated primary amines are sold by the Texaco Chemical Company under the tradename of "Jeffamine".
  • Jeffamine M-600 has the following structure: As seen from the structural formula above, Jeffamine M-600 contains both ethoxy and propoxy groups and is reported to have more than 1.71 meq/g of primary amine.
  • Another Jeffamine product having a mixture of ethoxy and propoxy groups is Jeffamine M-1000 which has the following structure: As seen from the use of fractional subscripts in the structural formula above, Jeffamine M-1000 is a mixture of linear polyether amines varying somewhat in their total ethoxy and propoxy groups.
  • Jeffamine M-1000 is reported to have a total amine content of 0.85 meq/g and a primary amine content of 0.83 meq/g.
  • Jeffamine M-300 and Jeffamine M-360 both contain a reasonably significant hydrocarbon group.
  • Jeffamine M-300 has the structure of: wherein R4 is a mixture of linear C10 to C12 alkyl groups and x has an average value of 1.
  • Jeffamine M-360 has the structure of: and has a total amine content of greater than 2.47 meq/g and a primary amine content of greater than 2.39 meq/g.
  • alkoxylated primary amines are sold by the Texaco Chemical Company under the tradename of "Surfonamine MNPA" (Surfonamine is a trademark of the Texaco Chemical Company) and this series of alkoxylated amines has the general structural formula of: wherein m, the number of ethoxy radicals per molecule,varies from about 1 to about 12, and n, the number of propoxy radicals per molecule, varies from about 1 to about 4, for the various amines of the series, i.e. , Surfonamine MNPA-380, 510, 750, and 860. These nonylphenol alkoxylated primary amines contain both a hydrocarbon chain and an aromatic radical, in addition to the alkoxy and amine radicals.
  • alkoxylated amine is meant herein generally an amine, either primary or secondary, having at least on alkoxy radical, either ethoxy or propoxy, within its chemical structure.
  • the alkoxylated amine is an amine wherein the alkoxy radical(s) comprise at least one percent of the amine's formula weight.
  • the alkoxylated amine is an amine wherein the alkoxy radical(s) comprise at least five percent of the amine's formula weight, and in even more preferred embodiment, at least ten percent of the amine's formula weight.
  • a useful group of hydrophobic radical containing amines are the aliphatic amines commercial available under the tradename of "Armeen” from Armak Chemicals ("Armeen” is a registered trademark of Akzo Chemie America for the aliphatic amines produced by Armak Chemicals).
  • Armeen primary amines are soyaamine (C18H35NH2) sold under the tradenames of Armeen S and Armeen SD.
  • Armeen SD has a water solubility (in percent of solution weight) of about 10.13 at 50° C and 4.01 at 80° C. It has a primary amine content of 98% and a secondary amine content of 2% (ASA).
  • Armeen primary amines are Armeen HTD, a hydrogenated tallow amine (C18H37NH2) having a water solubility of 4.39 at 80° C (a nonfluid mixture in water at 60° C),Armeen 16D, a hexadecylamine (C16H33NH2) which has a water solubility of 12.99 at 60° C. and 5.47 at 80° C, and Armeen 12D, a dodecylamine (C12H25NH2), which is a liquid at 25° C, and has a water solubility of 24.35 at 50° C and 12.50 at 80° C.
  • C18H37NH2 a hydrogenated tallow amine having a water solubility of 4.39 at 80° C (a nonfluid mixture in water at 60° C)
  • Armeen 16D a hexadecylamine (C16H33NH2) which has a water solubility of 12.99 at 60° C. and 5.47 at 80° C
  • Armeen secondary amines are Armeen 2C, a dicocoamine (C12H25)2NH, a solid at 25° C,and Armeen 2HT, a di(hydrogenated-tallow)amine, (C18H37)2NH2, which is also solid at 25° C.
  • the (trans)amidation process is conducted in an aqueous medium.
  • the use of an aqueous medium is generally less expensive than a nonaqueous medium.
  • the end product polymer is easier to isolate from an aqueous medium.
  • An aqueous medium moreover minimizes the toxicity of the reaction mixture, and the toxicity of the end product polymer if not completely isolated from the reaction medium.
  • the end product polymer isolation step may not be required. While all of such advantages ensue from the use of an aqueous reaction medium, the employment of an aqueous reaction medium heretofore would generally be considered contrary to the objectives of obtaining a reasonable degree of derivatization and an economically efficient process.
  • the present invention does not, in its broadest definition, exclude the use of nonaqueous reaction mediums, for instance dimethyl sulfoxide (“DMS”) or various other organic liquids.
  • DMS dimethyl sulfoxide
  • the reactants should be soluble or substantially homogeneously dispersible in the reaction medium employed, given the concentrations of reactants used.
  • Hydrophobe-containing amine reactants having some degree of carbon-to-carbon unsaturation within the hydrophobic moiety are generally more fluid than the equivalent fully saturated amines and such fluidity facilitates dispersing such reactants in the reaction medium, particularly when the medium is water.
  • concentration of the reactants in such process can of course be lowered if needed for to disperse the reactants.
  • the water solubility or water dispersibility characteristics of the starting material polymer are dependent upon the balance between its hydrophobic and hydrophilic pendant groups, and its molecular weight, and thus while in some instances one can select the starting material polymer so as to provide the desired degree of water solubility, in other instances the preference for a given polymer is an overriding factor.
  • a preferred concentration of the polymer in the reaction mixture is at least ten weight percent, more preferably twenty weight percent.
  • the starting reaction mixture need not even be fluid at room temperature.
  • the end product polymer even when an aqueous reaction medium is employed may possibly not be water soluble or water dispersible.
  • the (trans)amidation reaction is conducted at elevated temperatures and preferably under pressures that exceed atmospheric pressure.
  • the reaction generally is accomplished in a closed vessel at a temperature of from about 120° C. to about 200° C.
  • the starting material polymer may contain participating pendant groups that are wholly acid amide groups, for instance the pendant groups of (meth)acrylamide mer units, or that are wholly carboxylic groups, for instance the pendant groups of (meth)acrylic acid or maleic anhydride mer units. If the former situation existed, the process would be considered a transamidation reaction whereby acid amide groups are derivatized by amine reactants to N-substituted acid amide groups. If the latter situation existed, the process would be considered an amidation reaction whereby carboxylic groups would be derivatized by amine reactants to N-substituted acid amide groups. Hence the process is deemed a (trans)amidation reaction, and it has been found that the derivatization proceeds extremely efficiently when the starting material polymer contains a mixture of both carboxylic groups and acid amide groups.
  • the derivatization reaction generally does not proceed to the exhaustion of all of the derivatizing amine employed, and hence it is desirable to use a greater charge of amine reactant than stoichiometrically required for the desired degree of derivatization.
  • a one to one mole ratio of participating polymer pendant groups to derivatizing amine possibly may be used, and in fact less participating pendant groups and amine reactant, on a mole basis, may be reasonably used.
  • the derivatization reaction should be permitted to proceed for at least a one-half hour duration, and preferably for a time period of from about three to about eight hours.
  • the derivatization process was conducted using a concentration of starting material polymer of from about 20 to about 32 weight percent based on the entire reaction mixture (polymer, derivatizing agent and water medium).
  • concentration of starting material polymer on such basis is at least 20 weight percent, although a reasonably efficient process ensues when the concentration of the starting material polymer is as low as 10 weight percent, same basis.
  • concentration of starting material polymer may fall to as low as 5 weight percent or less.
  • the concentration of the end material polymer in the reaction mixture is of course dependent on the amount of derivatizing agent employed and the degree of reaction, in addition to the initial polymer concentration.
  • the starting material polymer's concentration was about 31 weight percent
  • the end material polymer's concentration was about 43 weight percent.
  • the starting material polymer must contain pendant groups having the structure of Formula I above.
  • Such pendant groups contain either a carboxylic radical (wherein X of Formula I is -OH and/or -O ⁇ ) or an acid amide radical (wherein X of Formula I is -NH2).
  • the mole ratio of carboxylic radical containing pendant groups to acid amide containing pendant groups in the starting material polymer is at most 1:9, and in more preferred embodiment is at most 1:3.
  • the unique polymers of the present invention contain both hydrophobic and alkoxylated groups which are substituents to the nitrogen of pendant acid amide groups.
  • the presence of these diverse groups within the same polymer provides unique characteristics for various end use applications. For instance, when used in water systems, both types of pendant groups may have a propensity to attach to substrates.
  • the hydrophobic moieties will tend to attach to substrates by virtue of their hydrophobic nature, while the alkoxylated moieties may tend to attach to substrate surfaces due to hydrogen bonding mechanisms.
  • the presence of both types of side chains provides unique thickening characteristics.
  • the polymer may contain as little as 0.1 mole percent of each type of group, based on total moles of mer units in the polymer.
  • the polymer contains at least 1 mole percent of each type of group (hydrophobic moiety and alkoxylated moiety), based on total moles of mer units in the polymer.
  • the polymer contains at least 2.5 mole percent of each type of group, same basis.
  • the molecular weight of the starting material pre-existing polymer is limited to about no more than 200,000, and in some instances, for instance if a homopolymer of acrylamide is used, to no more than 100,000 (weight average molecular weight).
  • the starting material polymer is of rather low molecular weight, for instance no more than 50,000, and more preferably no more than about 25,000, and the preference for such low molecular weight starting material preexisting polymers is particularly germane to the unique polymers having both hydrophobic and alkoxylated groups from which unique end use characteristics flow.
  • the molecular weight of the starting material polymer is at least about 2,000 (weight average molecular weight).
  • the degree of derivatization desired is to incorporate at least 0.1 mole percent of derivatized groups into the polymer, based on total moles of mer units in the polymer, and more preferably to incorporate at least 1 mole percent of the derivatized groups into the polymer, same basis.
  • the mole ratio of reactants, i.e. , pendant polymer groups having the structure of Formula I above (participating pendant groups) to the amine-containing derivatizing agent(s) is from about 50:1 to about 1:2, and in more preferred embodiment is from about 50:1 to about 1:1.
  • An acrylic acid/acrylamide copolymer having a weight average molecular weight of about 16,000 was derivatized by reaction with both soya-amine and an alkoxylated amine (primary amine) in a single reaction as follows. To 165 grams of a 35 weight percent aqueous solution of the copolymer was added 11.9 grams of the soya-amine (Armeen S) and 40.38 grams of the alkoxylated amine (Jeffamine M-1000 which is described above). This admixture was placed into a 300 ml. Parr reactor. The reactor was purged with nitrogen, then sealed, heated internally to 150° C., and held at that temperature for a 5 hour reaction period.
  • the reaction mixture recovered from the cooled reactor had a paste-like consistency. Based on L.C. analysis for residual amine, the soya-amine was determined to have reacted to the extent of 95 weight percent of its initial charge, and the alkoxylated amine was determined to have reacted to the extent of 83 weight percent of its initial charge.
  • Example 1 was repeated except the amount of the copolymer solution was decreased to 135 grams, the charge of the soya-amine was increased to 18.31 grams, and the charge of the alkoxylated amine was increased to 66.08 grams.
  • the reaction mixture recovered was again of paste-like consistency. Based on L.C. analysis for residual amine, the soya-amine was determined to have reacted to the extent of 86 weight percent of its initial charge and the alkoxylated amine was determined to have reacted to the extent of 58 weight percent of its initial charge.
  • An acrylamide homopolymer having a weight average molecular weight of about 7,500 was derivatized as follows. To 170 grams of a 33 weight percent aqueous solution of the polyacrylamide was added 39.51 grams of Jeffamine M-1000 and 10.94 grams of Armeen S, both of which are described above. These amounts were a 5 mole percent charge of both the Jeffamine M-1000 and Armeen S based on the total number of mer units in the polymer charge. This admixture was placed into a 300 ml. Parr reactor. The reactor was purged with nitrogen, then sealed, heated internally to 150° C., and held at that temperature for a 5 hour reaction period. The reaction mixture recovered from the cooled reactor was a brown liquid. Based on L.C. analysis for residual amine, the soya-amine (Armeen S) was determined to have reacted to the extent of 38 weight percent of its initial charge, and the alkoxylated amine was determined to have reacted to zero weight percent of its initial charge.
  • Example 3 was repeated except the amount of the polyacrylamide solution was decreased to 135 grams, and the mole percent charges of both the soya-amine and alkoxylated amine were increased to 10 mole percent (62.75 grams of Jeffamine M-1000 and 17.38 grams of Armeen S).
  • the reaction mixture recovered again was a brown liquid, and based on L.C. analysis for residual amine, the soya-amine was determined to have reacted to the extent of 34 weight percent of its initial charge and the alkoxylated amine was determined to have reacted to the extent of zero weight percent of its initial charge.
  • the present invention is applicable to the industries requiring agents for thickening and soil release, wherein the polymers having pendant hydrophobic and alkoxylated groups are useful.

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Claims (24)

  1. Verfahren zur Herstellung eines Polymers mit am Polymer-Rückgrat gebundenen Seitengruppen der Strukturformel:
    Figure imgb0013
     worin n = 0 oder eine ganze Zahl von 1 bis 10 ist, R¹ (bei Betrachtung des Polymers als Ganzes) ein Gemisch aus hydrophoben und alkoxylierten Resten ist und R Wasserstoff oder ein anderer Substituent als Wasserstoff ist, umfassend:
    das zumindest im wesentlichen homogene Dispergieren eines bereits bestehenden Polymers und zumindest eines Amins in einem Reaktionsmedium zur Bildung eines im wesentlichen homogenen Reaktionsgemisches,
    wobei das bereits bestehende Polymer beteiligte Seitengruppen der folgenden Strukturformel aufweist
    Figure imgb0014
     worin n wie oben definiert ist und X = -NH₂, -OH oder -O⁻ ist, sowie Salze und Gemische davon,
    wobei das Amin aus mit hydrophoben und alkoxylierten Resten mischsubstituierten primären und/oder sekundären Aminen besteht,
    und das Umsetzen des bereits bestehenden Polymers mit dem Amin bei erhöhter Temperatur und über eine Zeitspanne, die ausreicht, um zumindest einige der beteiligten Seitengruppen des bereits bestehenden Polymers mit den Aminen zu (trans)amidieren.
  2. Verfahren nach Anspruch 1, worin das Reaktionsmedium wäßrig ist.
  3. Verfahren nach Anspruch 1 oder 2, worin das bereits bestehende Polymer zumindest 10 Mol-% Mereinheiten enthält, die die beteiligten Seitengruppen aufweisen.
  4. Verfahren nach einem der vorhergehenden Ansprüche, worin der hydrophobe Rest zumindest drei Kohlenstoffatome enthält.
  5. Verfahren nach Anspruch 4, worin der hydrophobe Reste zumindest zwölf Kohlenstoffatome enthält.
  6. Verfahren nach einem der vorhergehenden Ansprüche, worin das Amin im wesentlichen primäres Amin ist.
  7. Verfahren nach einem der vorhergehenden Ansprüche, worin das Amin mit alkoxylierten Substituenten ein Amin ist, worin die Alkoxyreste zumindest 5% des Formelgewichts des Amins ausmachen.
  8. Verfahren nach Anspruch 7, worin die Alkoxyreste zumindest 10% des Formelgewichts des Amins ausmachen.
  9. Verfahren nach einem der vorhergehenden Ansprüche, worin die Konzentration des bereits bestehenden Polymers im Reaktionsgemisch zumindest 10 Gew.-% beträgt.
  10. Verfahren nach Anspruch 9, worin die Konzentration des bereits bestehenden Polymers im Reaktionsgemisch zumindest 20 Gew.-% beträgt.
  11. Verfahren nach einem der vorhergehenden Ansprüche, worin das Molverhältnis der beteiligten Seitengruppen mit einer Formel, worin X = -OH und/oder -O⁻ ist, zu den beteiligten Seitengruppen mit einer Formel, worin X = -NH₂ ist, zumindest 1:9 beträgt.
  12. Verfahren nach Anspruch 11, worin das Molverhältnis zumindest 1:3 beträgt.
  13. Verfahren nach einem der vorhergehenden Ansprüche, worin zumindest 0,1 Mol-% oder des Gemisches aus hydrophoben und alkoxylierten Resten, bezogen auf die gesamten Mereinheiten, in das vorliegende Polymer substituiert werden.
  14. Verfahren nach einem der vorhergehenden Ansprüche, worin das Molverhältnis der beteiligten Seitengruppen zum Amin im Reaktionsgemisch etwa 50:1 bis etwa 1:2 beträgt.
  15. Verfahren nach einem der vorhergehenden Ansprüche, worin das bereits bestehende Polymer ein durchschnittliches Molekulargewicht von bis zu 50.000 aufweist.
  16. Verfahren nach einem der vorhergehenden Ansprüche, worin das vorliegende Polvmer ein Polymer ist, das Acrylsäure- und Acrylamid-Mereinheiten enthält.
  17. Polymer mit Seitengruppen der Strukturformeln
    Figure imgb0015
     und
    Figure imgb0016
     worin n = 0 oder eine ganze Zahl von 1 bis 10 ist, R' ein hydrophober Rest ist, R" ein alkoxylierter Rest ist und R Wasserstoff oder ein anderer Substituent als Wasserstoff ist.
  18. Polymer nach Anspruch 17, worin der hydrophobe Rest zumindest drei Kohlenstoffatome enthält.
  19. Polymer nach Anspruch 18, worin der hydrophobe Rest zumindest zwölf Kohlenstoffatome enthält.
  20. Polymer nach einem der Ansprüche 17 bis 19, worin die Alkoxyreste innerhalb des alkoxylierten Rests zumindest 5% des Formelgewichts des alkoxylierten Rests ausmachen.
  21. Polymer nach einem der Ansprüche 17 bis 20, worin das Polymer zumindest 1 Mol% an Mereinheiten mit den einen hydrophoben Rest enthaltenden Seitengruppen und zumindest 1 Mol-% an Mereinheiten mit den einen alkoxylierten Rest enthaltenden Seitengruppen enthält.
  22. Polymer nach Anspruch 21, worin das Polymer zumindest 2,5 Mol-% an Mereinheiten mit den einen hydrophoben Rest enthaltenden Seitengruppen und zumindest 2,5 Mol-% an Mereinheiten mit den einen alkoxylierten Rest enthaltenden Seitengruppen enthält.
  23. Polymer nach einem der Ansprüche 17 bis 22, worin das Molekulargewicht des Polymers ohne hydrophobe und alkoxylierte Reste bis zu 50.000 beträgt.
  24. Polymer nach einem der Ansprüche 17 bis 23, worin das Molekulargewicht des Polvmers ohne hydrophobe und alkoxylierte Reste bis zu 25.000 beträgt.
EP91306039A 1990-07-06 1991-07-03 Synthese von hydrophoben alkoxylierten Polymeren Expired - Lifetime EP0466392B1 (de)

Applications Claiming Priority (2)

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US548838 1983-11-04
US07/548,838 US5075390A (en) 1990-07-06 1990-07-06 Synthesis of hydrophobic/alkoxylated polymers

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EP0466392A2 EP0466392A2 (de) 1992-01-15
EP0466392A3 EP0466392A3 (en) 1992-06-17
EP0466392B1 true EP0466392B1 (de) 1996-05-15

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US6383458B1 (en) 1991-07-10 2002-05-07 Newmont Mining Corporation Biooxidation process for recovery of metal values from sulfur-containing ore materials
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Also Published As

Publication number Publication date
US5075390A (en) 1991-12-24
EP0466392A2 (de) 1992-01-15
EP0466392A3 (en) 1992-06-17
ES2089135T3 (es) 1996-10-01
DE69119490T2 (de) 1996-10-31
DE69119490D1 (de) 1996-06-20

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